US5145925A - Chlorotrifluoroethylene/perfluoro(alkyl vinyl ether) copolymer - Google Patents
Chlorotrifluoroethylene/perfluoro(alkyl vinyl ether) copolymer Download PDFInfo
- Publication number
- US5145925A US5145925A US07/680,112 US68011291A US5145925A US 5145925 A US5145925 A US 5145925A US 68011291 A US68011291 A US 68011291A US 5145925 A US5145925 A US 5145925A
- Authority
- US
- United States
- Prior art keywords
- perfluoro
- vinyl ether
- copolymer
- chlorotrifluoroethylene
- alkyl vinyl
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F214/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen
- C08F214/18—Monomers containing fluorine
- C08F214/24—Trifluorochloroethene
- C08F214/242—Trifluorochloroethene with fluorinated vinyl ethers
Definitions
- the present invention relates to a chlorotrifluoroethylene/perfluoro(alkyl vinyl ether) copolymer.
- the present invention relates to a chlorotrifluoroethylene/perfluoro(alkyl vinyl ether) copolymer which contains the perfluoro(alkyl vinyl ether) in a specific amount and has a specific melt flow rate.
- polychlorotrifluoroethylene is a fluororesin having good moisture proof properties, transparency or mechanical strength, it is widely used for various purposes. For example, it is molded in a pipe form and used as a level gage, or it is used as a moisture-proof film.
- polychlorotrifluoroethylene when used, is very easily crystallized, and loses its transparency or becomes brittle as time passes. Crystallization polychlorotrifluoroethylene is prevented by copolymerization with vinylidene fluoride. However, in this case, when an amount of vinylidene fluoride is too small, the crystallization is not prevented, while when the amount of vinylidene fluoride is too large, a melting point of a copolymer is decreased or mechanical strength of the copolymer is greatly deteriorated.
- An object of the present invention is to provide a copolymer of chlorotrifluoroethylene which does not suffer from decrease of a melting point or deterioration of mechanical strength and can prevent crystallization advantageously.
- a copolymer which comprises chlorotrifluoroethylene and 0.01 to 1% by mole of perfluoro(alkyl vinyl ether) of the formula:
- R f is a C 3 --C 6 perfluoroalkyl group, and has a melt flow rate of 0.01 to 200 ⁇ 10 -3 cc/sec.
- the perfluoro(alkyl vinyl ether) to be copolymerized with chlorotrifluoroethylene according to the present invention is an ether of the formula (I).
- the perfluoroalkyl group R f of the formula (I) has 3 to 6 carbon atoms and may optionally have at least one substituent.
- Specific examples of the perfluoroalkyl group are a perfluoropropyl group, a perfluorobutyl group, a perfluoro(propoxypropyl) group, and the like. In view of easy availability and low cost, perfluoro(propyl vinyl ether) is preferred.
- the content of the perfluoro(alkyl vinyl ether) (I) in the copolymer is from 0.01 to 1% by mole.
- the content of the perfluoro(alkyl vinyl ether) is increased, the crystallization of the copolymer can be effectively prevented but the melting point of the polymer is decreased and the copolymer becomes soft so that the mechanical strength is deteriorated.
- the content of perfluoro(alkyl vinyl ether) is from 0.05 to 0.5% by mole.
- the copolymer of the present invention may be prepared by a per se conventional method.
- the copolymerization is carried out in an autoclave equipped with a stirrer.
- aqueous suspension polymerization is employed.
- a weight ratio of water to chlorotrifluoroethylene is from 1/10 to 10/1.
- a polymerization temperature is from 0° to 100° C., preferably from 5° to 30° C.
- a polymerization pressure is determined by a vapor pressure of chlorotrifluoroethylene and in turn the polymerization temperature.
- a weight of the perfluoro(alkyl vinyl ether) (I) to be copolymerized depends on the type of the perfluoro(alkyl vinyl ether) (I).
- a method for the changing of the perfluoro(alkyl vinyl ether) (I) is not critical, and all of the perfluoro(alkyl vinyl ether) (I) may be added to the reaction system in an initial stage or may be added portionwise or continuously.
- organic peroxide As a polymerization initiator, an organic peroxide is preferably used.
- organic peroxides to improve heat stability of the produced copolymer, organic peroxides of the following formulas are preferably used:
- n is an integer of 1 to 5
- n is an integer of 1 to 5
- X is a hydrogen atom, a fluorine atom or a chlorine atom.
- composition and properties of the copolymer are measured as follows:
- the content of the perfluoro(alkyl vinyl ether) is measured by 19 F FT-NMR of a solution of the copolymer in benzotrifluoride. That is, the content of the perfluoro(alkyl vinyl ether) is calculated from a ratio of an integrated strength of a peak assigned to the side chain perfluoro(alkyl ether) groups to those of other peaks from 19 F NMR spectrum.
- a melt flow rate is measured by extruding a melt of the copolymer from a nozzle having a diameter of 1 mm and a length of 1 mm under a load of 100 kg/cm 2 at 230° C.
- a sample having a length of 60 mm and a width of 8 mm is cut out and heated in an electric furnace at 100° C. for one hour to prepare a test sample.
- Each sample is bent by a bending modulus tester with increasing a bending angle by 10 degrees, and an angle at which the sample is first whitened on bending is measured as a whitening start angle.
- the larger whitening start angle means better suppression of crystallization.
Abstract
A copolymer comprising chlorotrifluoroethylene and 0.01 to 1% by mole of perfluoro(alkyl vinyl ether) of the formula:
R.sub.f --O--CF═CF.sub.2 (I)
wherein Rf is a C3 -C6 perfluoroalkyl group, and having a melt flow rate of 0.01 to 200×10-3 cc/sec., which has good mechanical strength and sufficiently high melting point.
Description
1. Field of the Invention
The present invention relates to a chlorotrifluoroethylene/perfluoro(alkyl vinyl ether) copolymer. In particular, the present invention relates to a chlorotrifluoroethylene/perfluoro(alkyl vinyl ether) copolymer which contains the perfluoro(alkyl vinyl ether) in a specific amount and has a specific melt flow rate.
2. Background Information
Since polychlorotrifluoroethylene is a fluororesin having good moisture proof properties, transparency or mechanical strength, it is widely used for various purposes. For example, it is molded in a pipe form and used as a level gage, or it is used as a moisture-proof film.
Since polychlorotrifluoroethylene, when used, is very easily crystallized, and loses its transparency or becomes brittle as time passes. Crystallization polychlorotrifluoroethylene is prevented by copolymerization with vinylidene fluoride. However, in this case, when an amount of vinylidene fluoride is too small, the crystallization is not prevented, while when the amount of vinylidene fluoride is too large, a melting point of a copolymer is decreased or mechanical strength of the copolymer is greatly deteriorated.
An object of the present invention is to provide a copolymer of chlorotrifluoroethylene which does not suffer from decrease of a melting point or deterioration of mechanical strength and can prevent crystallization advantageously.
According to the present invention, there is provided a copolymer which comprises chlorotrifluoroethylene and 0.01 to 1% by mole of perfluoro(alkyl vinyl ether) of the formula:
R.sub.f --O--CF═CF.sub.2 ( I)
wherein Rf is a C3 --C6 perfluoroalkyl group, and has a melt flow rate of 0.01 to 200 × 10-3 cc/sec.
The perfluoro(alkyl vinyl ether) to be copolymerized with chlorotrifluoroethylene according to the present invention is an ether of the formula (I). The perfluoroalkyl group Rf of the formula (I) has 3 to 6 carbon atoms and may optionally have at least one substituent. Specific examples of the perfluoroalkyl group are a perfluoropropyl group, a perfluorobutyl group, a perfluoro(propoxypropyl) group, and the like. In view of easy availability and low cost, perfluoro(propyl vinyl ether) is preferred.
The content of the perfluoro(alkyl vinyl ether) (I) in the copolymer is from 0.01 to 1% by mole.
When the content of the perfluoro(alkyl vinyl ether) is increased, the crystallization of the copolymer can be effectively prevented but the melting point of the polymer is decreased and the copolymer becomes soft so that the mechanical strength is deteriorated. Preferably, the content of perfluoro(alkyl vinyl ether) is from 0.05 to 0.5% by mole.
When the content of perfluoro(alkyl vinyl ether) exceeds 1% by mole, a polymerization rate is decreased to 50% or less of a homopolymerization rate of chlorotrifluoroethylene. Such low polymerization rate is uneconomical, or at such low polymerization rate, a polymerization degree may not be increased.
The copolymer of the present invention may be prepared by a per se conventional method. In general, the copolymerization is carried out in an autoclave equipped with a stirrer. Preferably, aqueous suspension polymerization is employed. In this case, a weight ratio of water to chlorotrifluoroethylene is from 1/10 to 10/1. A polymerization temperature is from 0° to 100° C., preferably from 5° to 30° C. A polymerization pressure is determined by a vapor pressure of chlorotrifluoroethylene and in turn the polymerization temperature.
A weight of the perfluoro(alkyl vinyl ether) (I) to be copolymerized depends on the type of the perfluoro(alkyl vinyl ether) (I). A method for the changing of the perfluoro(alkyl vinyl ether) (I) is not critical, and all of the perfluoro(alkyl vinyl ether) (I) may be added to the reaction system in an initial stage or may be added portionwise or continuously.
As a polymerization initiator, an organic peroxide is preferably used. Among the organic peroxides, to improve heat stability of the produced copolymer, organic peroxides of the following formulas are preferably used:
[Cl(CF.sub.2 CFCl).sub.m --CF.sub.2 COO].sub.2
wherein m is an integer of 1 to 5, and
[X(CF.sub.2 CF.sub.2).sub.n COO].sub.2
wherein n is an integer of 1 to 5, and X is a hydrogen atom, a fluorine atom or a chlorine atom.
In the present invention, the composition and properties of the copolymer are measured as follows:
The content of the perfluoro(alkyl vinyl ether) is measured by 19 F FT-NMR of a solution of the copolymer in benzotrifluoride. That is, the content of the perfluoro(alkyl vinyl ether) is calculated from a ratio of an integrated strength of a peak assigned to the side chain perfluoro(alkyl ether) groups to those of other peaks from 19 F NMR spectrum.
By using a KOKA-Type flow tester, a melt flow rate is measured by extruding a melt of the copolymer from a nozzle having a diameter of 1 mm and a length of 1 mm under a load of 100 kg/cm2 at 230° C.
From a sheet which is molded by heat press and has a thickness of 1 mm, a sample having a length of 60 mm and a width of 8 mm is cut out and heated in an electric furnace at 100° C. for one hour to prepare a test sample. Each sample is bent by a bending modulus tester with increasing a bending angle by 10 degrees, and an angle at which the sample is first whitened on bending is measured as a whitening start angle. The larger whitening start angle means better suppression of crystallization.
The present invention will be illustrated by following Examples, in which "parts" are by weight.
In a jacketed polymerization reactor equipped with a stirrer which could contain 4000 parts of water, deionized deaerated water (1000 parts) and sodium hydrogencarbonate (0.75 part) were charged. After replacing the interior atmosphere with pure nitrogen gas, the nitrogen gas was evacuated under reduced pressure. Then, chlorotrifluoroethylene (1000 parts), perfluoro(propyl vinyl ether) (10 parts) and carbon tetrachloride (10 parts) were injected under pressure. After adjusting the interior temperature at 20° C., stirring was started. To the stirred mixture, a solution of [Cl(CF2 CFCl)2 --CF2 COO]2 in trichlorotrifluoroethane (0.3 g/ml) (13 parts) was added as a polymerization initiator to initiate polymerization. After 24 hours polymerization, unreacted chlorotrifluoroethylene was purged, and a resulting copolymer was recovered, washed with warm water and dried to obtain powdery copolymer (370 parts).
A composition and properties of the copolymer are shown in the Table.
In the same manner as in Example 1 but charging 107 parts of perfluoro(propyl vinyl ether) and no carbon tetrachloride, polymerization was carried out to obtain a powdery copolymer (240 parts).
A composition and properties of the copolymer are shown in the Table.
In the same manner as in Example 1 but charging 244 parts of perfluoro(propyl vinyl ether) and no carbon tetrachloride, polymerization was carried out to obtain a powdery copolymer (120 parts).
A composition and properties of the copolymer are shown in the Table.
In a jacketed polymerization reactor equipped with a stirrer which could contain 4000 parts of water, deionized deaerated water (1000 parts) and sodium hydrogencarbonate (0.75 part) were charged. After replacing the interior atmosphere with pure nitrogen gas, the nitrogen gas was evacuated under reduced pressure. Then, chlorotrifluoroethylene (1000 parts), vinylidene fluoride (16 parts) and carbon tetrachloride (8 parts) were injected under pressure. After adjusting the interior temperature at 20° C., stirring was started. To the stirred mixture, a solution of [Cl(CF2 CFCl)2 --CF2 COO]2 in trichlorotrifluoroethane (the same concentration as in Example 1) (10 parts) was added as a polymerization initiator to initiate polymerization. During polymerization, vinylidene fluoride (10 parts) was additionally added over 48 hours to make the gas composition in the reactor constant, and after 24 hours from the start of the polymerization, the same solution of [Cl(CF2 CFCl)2 --CF2 COO]2 in trichlorotrifluoroethane as above (10 parts) was added. The total polymerization time was 48 hours. Thereafter, unreacted chlorotrifluoroethylene was purged, and a resulting copolymer was recovered, washed with warm water and dried to obtain powdery copolymer (580 parts).
A composition and properties of the copolymer are shown in the Table.
In a jacketed polymerization reactor equipped with a stirrer which could contain 4000 parts of water, deionized deaerated water (1000 parts) and sodium hydrogencarbonate (0.75 part) were charged. After replacing the interior atmosphere with pure nitrogen gas, the nitrogen gas was evacuated under reduced pressure. Then, chlorotrifluoroethylene (1000 parts) was injected under pressure. After adjusting the interior temperature at 20° C., stirring was started. To the stirred mixture, a solution of [Cl(CF2 CFCl)2 --CF2 COO]2 in trichlorotrifluoroethane (the same concentration as in Example 1) (3 parts) was added as a polymerization initiator to initiate polymerization. After 24 hours from the start of the polymerization, the same solution of [Cl(CF2 CFCl)2 --CF2 COO]2 in trichlorotrifluoroethane as above (1.5 parts) was added. The total polymerization time was 42 hours. Thereafter, unreacted chlorotrifluoroethylene was purged, and a resulting copolymer was recovered, washed with warm water and dried to obtain powdery copolymer (460 parts).
A composition and properties of the copolymer are shown in the Table.
TABLE
__________________________________________________________________________
Tensile properties*.sup.)
Example Melt flow rate
Melting
Heat of fusion
Crystallization
YS TS EL Whitening
No. Modifier (mol %)
(×10.sup.-3 cc/sec.)
point (°C.)
(cal/g)
temp. (kg/cm.sup.2)
(kg/cm.sup.2)
(%)
start angle
(°)
__________________________________________________________________________
1 Perfluoro-
27.6 213.5 5.22 174.0 424.7
257.2
49.5
60
(propyl vinyl
ether) (0.05)
2 ↑ (0.5)
2.65 201.0 3.04 164.0 389.4
262.3
61.5
90
Comp. 1
↑ (1.1)
27.6 189.5 2.45 146.0 368.2
269.2
139.8
90
Comp. 2
Vinylidene
59.0 193.5 4.61 153.0 367.8
219.7
64.2
60
fluoride
(4.0)
Comp. 3
-- 39.4 213.5 4.81 178.5 441.7
274.7
72.5
40
__________________________________________________________________________
Note:
*.sup.) YS: Yield Stress
TS: Tensile strength
EL: Elongation
Claims (4)
1. A copolymer which comprises chlorotrifluoroethylene and 0.01 to 1% by mole of perfluoro(alkyl vinyl ether) of the formula:
R.sub.f --O--CF═CF.sub.2 ( I)
wherein Rf is a C3 -C6 perfluoroalkyl group, and has a melt flow rate of 0.01 to 200 × 10-3 cc/sec.
2. The copolymer according to claim 1, wherein a content of said perfluro(alkyl vinyl ether) is 0.05 to 0.5% by mole.
3. The copolymer according to claim 1, wherein said perfluoro(alkyl vinyl ether) is perfluoro(propyl vinyl ether).
4. The copolymer according to claim 2, wherein said perfluoro(alkyl vinyl ether) is perfluoro(propyl vinyl ether).
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2-90894 | 1990-04-04 | ||
| JP2090894A JP2853254B2 (en) | 1990-04-04 | 1990-04-04 | Chlorotrifluoroethylene / perfluoro (alkyl vinyl ether) copolymer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US5145925A true US5145925A (en) | 1992-09-08 |
Family
ID=14011113
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US07/680,112 Expired - Lifetime US5145925A (en) | 1990-04-04 | 1991-04-03 | Chlorotrifluoroethylene/perfluoro(alkyl vinyl ether) copolymer |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US5145925A (en) |
| EP (1) | EP0450613B1 (en) |
| JP (1) | JP2853254B2 (en) |
| CA (1) | CA2039666C (en) |
| DE (1) | DE69122289T2 (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5495028A (en) * | 1993-07-05 | 1996-02-27 | Ausimont, S.P.A. | Perfluorodioxoles, the preparation process thereof, and homopolymers and copolymers obtained therefrom |
| US6277936B1 (en) | 1999-07-09 | 2001-08-21 | Auismont S.P.A. | Perhalogenated thermoplastic (CO)polymers of chlorotrifluoroethylene |
| US6391975B1 (en) | 1999-07-09 | 2002-05-21 | Ausimont S.P.A. | Thermoplastic perhalogenated (CO)polymers of chlorotrifluoroethylene |
| US20120184697A1 (en) * | 2006-12-20 | 2012-07-19 | Honeywell International Inc. | Copolymers for barriers |
| CN104130345A (en) * | 2014-07-07 | 2014-11-05 | 常熟市新华化工有限公司 | Preparation method of high-strength polychlorotrifluoroethylene |
| CN104892811A (en) * | 2014-03-07 | 2015-09-09 | 浙江省化工研究院有限公司 | Ethylene-trifluorochloroethylene copolymer with novel structure, and preparation method and application thereof |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2118926A1 (en) * | 1991-09-27 | 1993-04-01 | Russell L. Schneider | High barrier pctfe film |
| EP1741548B1 (en) | 2004-04-13 | 2018-12-19 | Daikin Industries, Ltd. | Fluid transfer member |
| JP4582091B2 (en) | 2004-04-13 | 2010-11-17 | ダイキン工業株式会社 | Chlorotrifluoroethylene copolymer |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2856435A (en) * | 1956-10-29 | 1958-10-14 | Minnesota Mining & Mfg | 1, 1 dihydrofluoroalkyl perfluoroallyl ethers |
| US3132123A (en) * | 1960-11-25 | 1964-05-05 | Du Pont | Polymers of perfluoroalkoxy perfluorovinyl ethers |
| US3180895A (en) * | 1960-11-25 | 1965-04-27 | Du Pont | Fluorocarbon ethers |
| US3752789A (en) * | 1971-08-20 | 1973-08-14 | Du Pont | Isolation of a fluoropolymer from a latex |
| US4262101A (en) * | 1976-08-31 | 1981-04-14 | Hoechst Aktiengesellschaft | Copolymers of tetrafluoroethylene and process for their manufacture |
| US4381384A (en) * | 1981-08-17 | 1983-04-26 | E. I. Du Pont De Nemours And Company | Continuous polymerization process |
| JPS59173110A (en) * | 1983-03-22 | 1984-10-01 | Sankyo Kasei Kogyo Kk | Composition of polymer flocculating agent |
| JPS59173109A (en) * | 1983-03-23 | 1984-10-01 | Nippon Mektron Ltd | Defoaming agent |
| US4587316A (en) * | 1983-02-01 | 1986-05-06 | Daikin Kogyo Co., Ltd. | Fluorine-containing copolymers and films thereof |
| USRE32199E (en) * | 1969-04-22 | 1986-07-08 | E. I. Du Pont De Nemours And Company | Tough, stable tetrafluoroethylene-fluoroalkyl perfluorovinyl ether copolymers |
| US4619983A (en) * | 1980-12-26 | 1986-10-28 | Asahi Glass Company Limited | Copolymer for fluorine-containing elastomer having excellent low temperature resistance and alcohol resistance |
-
1990
- 1990-04-04 JP JP2090894A patent/JP2853254B2/en not_active Expired - Fee Related
-
1991
- 1991-04-03 CA CA002039666A patent/CA2039666C/en not_active Expired - Fee Related
- 1991-04-03 US US07/680,112 patent/US5145925A/en not_active Expired - Lifetime
- 1991-04-04 DE DE69122289T patent/DE69122289T2/en not_active Expired - Fee Related
- 1991-04-04 EP EP91105309A patent/EP0450613B1/en not_active Expired - Lifetime
Patent Citations (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2856435A (en) * | 1956-10-29 | 1958-10-14 | Minnesota Mining & Mfg | 1, 1 dihydrofluoroalkyl perfluoroallyl ethers |
| US2975163A (en) * | 1956-10-29 | 1961-03-14 | Minnesota Mining & Mfg | Fluorine containing organic compounds and preparation thereof |
| US3132123A (en) * | 1960-11-25 | 1964-05-05 | Du Pont | Polymers of perfluoroalkoxy perfluorovinyl ethers |
| US3180895A (en) * | 1960-11-25 | 1965-04-27 | Du Pont | Fluorocarbon ethers |
| USRE32199E (en) * | 1969-04-22 | 1986-07-08 | E. I. Du Pont De Nemours And Company | Tough, stable tetrafluoroethylene-fluoroalkyl perfluorovinyl ether copolymers |
| US3752789A (en) * | 1971-08-20 | 1973-08-14 | Du Pont | Isolation of a fluoropolymer from a latex |
| US4262101A (en) * | 1976-08-31 | 1981-04-14 | Hoechst Aktiengesellschaft | Copolymers of tetrafluoroethylene and process for their manufacture |
| US4619983A (en) * | 1980-12-26 | 1986-10-28 | Asahi Glass Company Limited | Copolymer for fluorine-containing elastomer having excellent low temperature resistance and alcohol resistance |
| US4381384A (en) * | 1981-08-17 | 1983-04-26 | E. I. Du Pont De Nemours And Company | Continuous polymerization process |
| US4587316A (en) * | 1983-02-01 | 1986-05-06 | Daikin Kogyo Co., Ltd. | Fluorine-containing copolymers and films thereof |
| JPS59173110A (en) * | 1983-03-22 | 1984-10-01 | Sankyo Kasei Kogyo Kk | Composition of polymer flocculating agent |
| JPS59173109A (en) * | 1983-03-23 | 1984-10-01 | Nippon Mektron Ltd | Defoaming agent |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5495028A (en) * | 1993-07-05 | 1996-02-27 | Ausimont, S.P.A. | Perfluorodioxoles, the preparation process thereof, and homopolymers and copolymers obtained therefrom |
| US5498682A (en) * | 1993-07-05 | 1996-03-12 | Ausimont, S.P.A. | Perfluorodioxoles, the preparation process thereof, and homopolymers and copolymers obtained therefrom |
| US5571932A (en) * | 1993-07-05 | 1996-11-05 | Ausimont S.P.A. | Perfluorodioxoles, the preparation process thereof, and homopolymers and copolymers obtained therefrom |
| US5646223A (en) * | 1993-07-05 | 1997-07-08 | Ausimont S.P.A. | Perfluorodioxoles, the preparation process thereof, and homopolymers and copolymers therefrom |
| US6277936B1 (en) | 1999-07-09 | 2001-08-21 | Auismont S.P.A. | Perhalogenated thermoplastic (CO)polymers of chlorotrifluoroethylene |
| US6391975B1 (en) | 1999-07-09 | 2002-05-21 | Ausimont S.P.A. | Thermoplastic perhalogenated (CO)polymers of chlorotrifluoroethylene |
| US20120184697A1 (en) * | 2006-12-20 | 2012-07-19 | Honeywell International Inc. | Copolymers for barriers |
| CN104892811A (en) * | 2014-03-07 | 2015-09-09 | 浙江省化工研究院有限公司 | Ethylene-trifluorochloroethylene copolymer with novel structure, and preparation method and application thereof |
| CN104892811B (en) * | 2014-03-07 | 2017-12-01 | 浙江省化工研究院有限公司 | A kind of ethene chlorotrifluoroethylene, its preparation method and application |
| CN104130345A (en) * | 2014-07-07 | 2014-11-05 | 常熟市新华化工有限公司 | Preparation method of high-strength polychlorotrifluoroethylene |
Also Published As
| Publication number | Publication date |
|---|---|
| CA2039666C (en) | 2001-10-23 |
| DE69122289T2 (en) | 1997-03-13 |
| JPH03287614A (en) | 1991-12-18 |
| DE69122289D1 (en) | 1996-10-31 |
| EP0450613A1 (en) | 1991-10-09 |
| EP0450613B1 (en) | 1996-09-25 |
| CA2039666A1 (en) | 1991-10-05 |
| JP2853254B2 (en) | 1999-02-03 |
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